MODELING AND SIMULATION OF THE REVERSED FLOW OPERATION OF A FIXED-BED REACTOR FOR METHANOL SYNTHESIS

被引：65

作者：

VANDENBUSSCHE, KM ^{[1
]}

NEOPHYTIDES, SN ^{[1
]}

ZOLOTARSKII, IA ^{[1
]}

FROMENT, GF ^{[1
]}

机构：

[1] STATE UNIV GHENT,PETROCHEM TECH LAB,KRIJGSLAAN 281,B-9000 GHENT,BELGIUM

来源：

CHEMICAL ENGINEERING SCIENCE | 1993年 / 48卷 / 19期

关键词：

D O I：

10.1016/0009-2509(93)80150-O

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

The proposed simulation of the reversed flow operation of a fixed-bed reactor for methanol synthesis is based upon a heterogeneous one-dimensional model. Different levels of transient modelling are compared. By using the most sophisticated model, the influence of a number of operating parameters is assessed. Considerable insight into the reactor behaviour is obtained.

引用

页码：3335 / 3345

页数：11

共 32 条

[21] SAPUNDZHIEV K, 1988, TEOR OSNOVY KHIM TEK, V22, P349
[22] PERIODICAL OPERATION OF CHEMICAL PROCESSES AND EVALUATION OF CONVERSION IMPROVEMENTS
SCHADLICH, K
HOFFMANN, U
HOFMANN, H
[J]. CHEMICAL ENGINEERING SCIENCE, 1983, 38 (09) : 1375 - 1384
[23] SILVESTON PL, 1987, REACTORS REACTION EN
[24] THULLIE J, 1990, UNSTEADY STATE PROCE, P687
[25] VANDENBUSSCHE KM, 1992, P EC C ENERGY EFFICI
[26] VANDENBUSSCHE KM, IN PRESS
[27] VANDENBUSSCHE KM, 1992, 8TH P INT C LARG CHE
[28] Villadsen J., 1978, SOLUTION DIFFERENTIA
[29] MULTIFUNCTIONAL REACTORS
WESTERTERP, KR
[J]. CHEMICAL ENGINEERING SCIENCE, 1992, 47 (9-11) : 2195 - 2206
[30] REACTOR PERFORMANCE WITH PERIODIC-FLOW REVERSAL FOR A MULTISTEP COMPLEX-REACTION
ZAGORUIKO, AN
MATROS, YS
KUMAR, VR
KULKARNI, BD
[J]. CHEMICAL ENGINEERING SCIENCE, 1992, 47 (17-18) : 4315 - 4321

← 1 2 3 4 →